Molding compositions containing fillers and modified polybutylene terephthalate (PBT) random copolymers derived from polyethylene terephthalated (PET)
A technology of polyethylene terephthalate and polybutylene terephthalate, which is applied in the field of residues of ethylene terephthalate components, can solve the problems of non-supply and the like
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Embodiment 1
[0265] The modified polybutylene terephthalate random copolymer is derived from polyethylene terephthalate as follows. The clear PET bottle waste was obtained from commercial sources. In the waste cleaning process, the PET waste is manually cleaned, including first washing with hot water, then manually picking to separate colored bottles and PVC bottles, crushing, hydrofloatation to separate PP, labels, lids, etc., alkali Wash to remove the glue, finally wash with demineralized water to remove the alkali, and then dry. The obtained PET flake is used as the main raw material in the depolymerization step. The iv specification of PET flakes recovered after consumption is 0.68~0.78dl / g, and the melting point specification is 245~255℃. The PVC content is less than 10ppm in specification. Butylene glycol is obtained from BASF, and its purity specification is >99.5wt.%. Ethylene glycol is obtained from Merck, and its purity specification is >99.5 wt.%. The TPT catalyst used was a commerc...
Embodiment 2-5
[0280] Example 2-5: Glass-filled composition
[0281] A glass-filled composition having the specified amounts of ingredients as shown in Table 4 was prepared and tested.
[0282] Table 4
[0283] Component
Unit
Example 2
Example 3
(comparative example)
Example 4
Example 5
(comparative example) PET-derived PBT, (0.66iv) wt.% 16 - 35.52 - PET-derived PBT, (1.2iv) wt.% 32.4 - 35.44 - GE VIRGIN PBT 195(0.66iv) wt.% - 16 - 35.52 GE VIRGIN PBT 315(1.2iv) wt.% - 32.4 - 35.44 Standard 13 micron glass fiber wt.% 30 30 30 30 Polycarbonate 105, grade 100 powder wt.% 2 2 - - High fluidity polycarbonate-Lexan
ML8199-111N
wt.%
18
18
-
-
Hydrocarbon wax release agent wt.% 0.4 0.4 - - Phosphoric acid—sodium, anhydrous wt.% 0.2 0.2 - - Hindered phenol stabilizer (Irganox1010) wt.% 0.06 0.06 0.04 0.04 Linear Low Density Polyethylene...
Embodiment 2
[0287] At a barrel and die temperature of 240-265°C and a screw speed of 150-300 rpm, the ingredients of Example 2 as shown above were placed on an 89mm single-screw extruder with a vacuum vented mixing screw. Squeeze out. The extruder has 8 independent feeders for different raw materials, of which one downstream feeder is for glass, and the extruder can operate at a maximum rate of 600 lbs / hr (272.2 kg / hour). The extrudate was cooled in a water bath and then pelletized. The test parts were injection molded on a van Dom molding machine set at a temperature of about 240-265°C. Before injection, the pellets were dried in a forced air circulation oven at 120°C for 3-4 hours.
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